Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP4530320B2 - Microorganism immobilization carrier - Google Patents
[go: Go Back, main page]

JP4530320B2 - Microorganism immobilization carrier - Google Patents

Microorganism immobilization carrier Download PDF

Info

Publication number
JP4530320B2
JP4530320B2 JP2001152331A JP2001152331A JP4530320B2 JP 4530320 B2 JP4530320 B2 JP 4530320B2 JP 2001152331 A JP2001152331 A JP 2001152331A JP 2001152331 A JP2001152331 A JP 2001152331A JP 4530320 B2 JP4530320 B2 JP 4530320B2
Authority
JP
Japan
Prior art keywords
acid
carrier
microorganism
hours
fluidity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2001152331A
Other languages
Japanese (ja)
Other versions
JP2002346583A5 (en
JP2002346583A (en
Inventor
敬 奥村
渉 藤井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Mitsubishi Rayon Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Chemical Corp, Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Chemical Corp
Priority to JP2001152331A priority Critical patent/JP4530320B2/en
Publication of JP2002346583A publication Critical patent/JP2002346583A/en
Publication of JP2002346583A5 publication Critical patent/JP2002346583A5/ja
Application granted granted Critical
Publication of JP4530320B2 publication Critical patent/JP4530320B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Biological Treatment Of Waste Water (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、生化学的に排水処理を行う際に、表面に微生物を付着させて使用される微生物固定化担体に関する。
【0002】
【従来の技術】
生物学的排水処理方法の一つとして、微生物が付着された微生物固定化担体を槽内で流動させ、同担体の表面に付着している微生物により有機物や窒素を吸着、分解して処理する方法が用いられている。この微生物固定化担体としては、親水性ゲル、多孔質中空樹脂、ウレタンフォーム等が、用いられている。
【0003】
多孔質中空樹脂は、材料が安価である上、成形が容易なことから広く使用されている。この多孔質中空樹脂としては、ポリプロピレン、ポリエチレン、等があげられる。ポリプロピレンは、微生物の付着量を増やすため、発泡成形し、多孔質体として用いられることが多い。
しかしながら、多孔質中空樹脂からなる微生物固定化担体は、表面の疎水性が高く、しかも菌体を付着しやすくすることを目的として発泡成形等の手段で表面を粗化しているため、同担体を排水槽に投入した直後は、同担体の表面に気泡が付着して浮いてしまい、排水内に浸漬して流動し難く、良好な排水処理ができるようになるまでに長時間を要していた。
【0004】
したがって従来から担体表面の親水性を高める改良が多数提案されている。例えば特開昭63−302994号公報には、酸化可能な熱可塑性樹脂からなる粒状体をスルホクロム混合物(硫酸、重クロム酸カリ及び水)又は発煙硫酸のスルホナイト混合物と接触させることにより酸化して親水化する手法が開示されている。かかる酸化された粒状体からなる担体は、水との間の相互作用が向上され、担体の浮遊現象や担体体間の凝結が抑制される。
【0005】
また、特開昭58−198288号公報には、担体表面を濃硫酸によりエッチングすることにより、担体表面に凹凸を形成して微生物の付着性を向上させる手法が開示されている。
【0006】
【発明が解決しようとする課題】
しかしながら、前述した担体表面の親水化方法は、濃硫酸のように強力な酸化剤を用いるものであるため、処理する際、取り扱いに細心の注意を行わないと危険を伴うという問題があった。
【0007】
また、特開昭58−198288号公報のように、表面に凹凸が形成されるような過酷な条件で処理すると、担体が酸化され過ぎて耐久性に問題が生じる懸念があった。
【0008】
こうした問題を解決するために本発明は、酸処理の条件を適正な範囲に制御し、簡便で安価かつ安全に製造でき、使用開始後すぐに良好な流動性を有し、かつ耐久性に優れた担体を提供することを目的とする。
【0009】
【課題を解決するための手段】
すなわち本発明の要旨は、酸変性熱可塑性樹脂及び炭酸カルシウムを含む成型体を、0.1規定〜5規定の塩酸にて処理してなる流動性が向上した微生物固定化担体にある。
【0010】
また、前記成型体を酸に0.1〜10時間浸漬させると確実に流動性を改善できるため好ましい。
また、前記酸が塩酸であると取り扱い性に優れるため好ましい。
また、前記熱可塑性樹脂が酸変性熱可塑性樹脂を含むと、初期流動性が高くなるため好ましく、さらにプロピレン−無水マレイン酸共重合体又はエチレン−メタクリル酸共重合体(アイオノマー樹脂)を含むとより好ましい。
また、前記成型体中に占める前記酸変性熱可塑性樹脂の含有量が10重量%以上であると、初期流動性がより高くなるため好ましい。
また、前記成形体が中空円筒形状であると、微生物の付着性が向上するため好ましい。
また、前記成型体の比重が0.8〜1.2g/cmであると、流動性が向上するため好ましい。
また、固形分含量が1000mg/Lの液1L中に、前記微生物固定化担体を見かけ容積として100ml添加し、1L/minの流量で曝気したとき、曝気開始から5時間以内で前記微生物固定化担体の80%以上が前記液中を循環流動すると、排水処理装置の使用開始時の立ち上がりが早くなるため好ましい。
【0011】
【発明の実施の形態】
以下本発明の形態例を説明するが、本発明がそれらに限定解釈されるものではない。
【0012】
本発明に用いる熱可塑性樹脂は、ポリプロピレン、ポリエチレン、ポリ塩化ビニル、エチレン−酢酸ビニル共重合樹脂、ポリスチレン等があげられるが、これらに限定されるものではない。これらの熱可塑性樹脂は、1種または2種以上組み合わせて用いることができ、ポリプロピレン、ポリエチレンなどが特に好ましい。
【0013】
前述の熱可塑性樹脂と共に酸変性性熱可塑性樹脂を用いると、担体の流動性が更に向上するため好ましい。酸変性性熱可塑性樹脂としては、プロピレン−無水マレイン酸共重合体(例えば三井化学(株)製、商品名アドマー、三洋化成(株)製、商品名ユーメックス、三菱化学(株)製、商品名モディック)、エチレン−メタクリル酸共重合体(アイオノマー樹脂、例えば三井デュポンポリケミカル(株)製、商品名ハイミラン)、メタクリル酸メチル−メタクリル酸共重合体(三菱レイヨン(株)製、商品名アクリペット)等があげられる。酸変性熱可塑性樹脂は、1種または2種以上組み合わせて用いることができる。
酸変性ポリマーの含有量は、酸変成量にもよるが、十分な親水性を与えるためには10重量%以上とすることが好ましく、前記酸変性熱可塑性樹脂のみで担体を得ることもできる。
【0014】
本発明に用いる成型体は、上述の樹脂組成物を、従来から使用されている周知の方法により成型すればよく、例えば押出し機を用いて容易に製造することができ、格別の装置や後処理も不要となり、廉価に製造可能である。
成型の際、形状は必ずしも限定されず、円柱状、円筒状、球状、立方体状等にすることができるが、中空円筒状とすると、微生物の付着性が向上するため好ましい。
【0015】
また、他の成分として、炭酸カルシウム、タルク、ゼオライト、硫酸バリウム、酸化チタン、チタン酸カリウム、水酸化アルミニウム等の比重調整材や、多孔質化のためのアゾジカルボンアミド(ADCA)、ジニトロソペンタメチレンテトラミン(DPT)、炭酸系などの発泡剤、発泡助剤、さらには適当な添加剤を含んでいてもよい。
【0016】
本発明に用いる成型体の比重は、0.8〜1.2g/cmの範囲であることが好ましい。さらに、水中での流動性の点からは、1.00に近い方がより望ましい。成型体を上記比重に調整することにより、これを用いて製造した担体を流動床用として使用する場合に、好適な流動性が得られる。
【0017】
前述の成型体を、0.1〜5規定の酸を用いて酸処理することによって、担体の流動性を向上させることができる。使用する酸の濃度が0.1規定未満であると、担体の初期流動性は無処理の場合と同等であり、酸処理の効果は認められない。
一方5規定を超える濃度の酸で処理した場合、樹脂表面の侵食や溶出が起こりやすく、耐久性に問題が生じる可能性があることに加え、処理の際、取り扱いに厳重な注意を払わないと危険であるため好ましくない。
【0018】
使用する酸の種類は必ずしも限定はされず、硫酸、硝酸、塩酸、リン酸、酢酸等を用いることができるが、中でも塩酸は安価で処理の効果が高く、かつ取り扱い性に優れるため好ましい。
【0019】
処理条件は、前記成型体の表面が酸に接触するなら特に限定はされないが、酸溶液中に成型体を浸漬させると、簡便に処理できるため好ましい。浸漬する温度も特に限定されず、室温で処理すればよい。浸漬時間は、流動性向上の効果を十分に出すことと、生産性を併せて考慮すると、0.1〜10時間とすることが好ましく、0.5〜5時間とすることがより好ましい。
なお、浸漬処理の際は液を撹拌すると処理効率が向上するため好ましい。
【0020】
微生物固定化担体の流動性の評価としては、固形分含量が1000mg/Lの液1L中に、前記微生物固定化担体を見かけ容積として100ml添加し、1L/minの流量で曝気する方法により評価することができる。この試験において、曝気開始から5時間以内で前記微生物固定化担体の80%が前記液中を循環流動することが好ましい。この流動性試験において短時間で流動する担体は、実際の装置、例えば生物学的排水処理装置においても速やかに流動する。
なお、この流動性試験で言う固形分とは、例えば活性汚泥のように、水中の有機成分を代謝、分解する能力を持つ微生物群を含んだものを言い、その含量は蒸発残分の測定により求められる。砂粒、金属粉等の無機物のように、水中の有機成分を分解する能力を持たないものは、この流動性試験で言う固形分には含まれない。
【0021】
以下本発明の実施の形態について具体的な実施例及び比較例を挙げて詳細に説明する。
【0022】
1.成型体の製造方法
樹脂及び炭酸カルシウムを2軸同方向押出機を用いて混合し、ペレット状に成型した後、発泡剤としてアゾジカルボンアミドを加えて単軸押し出し機により押出成形を行い、外径5mm、内径3.5mm、長さ5mmの多孔性中空円筒状の成型体を得た。
なお、樹脂:炭酸カルシウム:発泡剤の重量比は、75:24:1とした。
【0023】
2.酸処理
前述の成型体を、酸溶液に25℃にて2時間、撹拌しながら浸漬させた。
【0024】
3.流動性試験
図1に示す水処理装置を用い、容量1リットルの槽にMLSS濃度1000mg/Lの汚泥と、見かけ体積100mlの担体を添加した。そして1L/minで空気を曝気しながら、人工排水を原水として負荷量0.4kg−COD/m3・日で馴養を行い、担体が流動するまでの時間を観察した。
【0025】
<実施例1>
樹脂としてポリプロピレン、酸として3規定塩酸を用いた。流動性試験の結果は、担体の80%が流動するのに要した時間は4時間であり、すべての担体が流動するのに要した時間は6時間であった。
【0026】
<実施例2>
樹脂としてプロピレン−無水マレイン酸共重合体、酸として3規定塩酸を用いた。流動性試験の結果は、担体の80%が流動するのに要した時間は2時間であり、すべての担体が流動するのに要した時間は3時間であった。
【0027】
<実施例3>
樹脂としてエチレン−メタクリル酸共重合体、酸として3規定塩酸を用いた。流動性試験の結果は、担体の80%が流動するのに要した時間は2時間であり、すべての担体が流動するのに要した時間は5時間であった。
【0028】
<実施例4>
樹脂としてポリプロピレン、酸として1規定塩酸を用いた。流動性試験の結果は、担体の80%が流動するのに要した時間は4時間であり、すべての担体が流動するのに要した時間は6時間であった。
【0029】
<比較例1>
樹脂としてポリプロピレンを用い、酸処理は行わなかった。流動性試験の結果は、担体の80%が流動するのに要した時間は36時間であり、すべての担体が流動するのに要した時間は48時間であった。
【0030】
<比較例2>
樹脂としてプロピレン−無水マレイン酸共重合体を用い、酸処理は行わなかった。流動性試験の結果は、担体の80%が流動するのに要した時間は8時間であり、すべての担体が流動するのに要した時間は12時間であった。
【0031】
<比較例3>
樹脂としてエチレン−メタクリル酸共重合体を用い、酸処理は行わなかった。流動性試験の結果は、担体の80%が流動するのに要した時間は8時間であり、すべての担体が流動するのに要した時間は12時間であった。
【0032】
以上の実施例及び比較例から分かるように、樹脂成型体を酸処理することにより、担体の流動性を向上させることができた。
【0033】
【発明の効果】
本発明によれば、熱可塑性樹脂を0.1〜5規定の酸によって処理することにより、良好な流動性を有し、かつ耐久性に優れた担体を簡便で安価かつ安全に得ることができる。
【図面の簡単な説明】
【図1】実施例で使用した水処理装置を示す概略図である。
【符号の説明】
10 水処理装置
11 スクリーン
12 担体
13 整流板
14 散気管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a microorganism-immobilized carrier used by attaching microorganisms to a surface when performing wastewater treatment biochemically.
[0002]
[Prior art]
One of the biological wastewater treatment methods is a method in which a microorganism-immobilized carrier to which microorganisms are attached flows in a tank, and organic matter and nitrogen are adsorbed and decomposed by microorganisms attached to the surface of the carrier. Is used. As this microorganism-immobilized carrier, hydrophilic gel, porous hollow resin, urethane foam and the like are used.
[0003]
Porous hollow resins are widely used because they are inexpensive and easy to mold. Examples of the porous hollow resin include polypropylene and polyethylene. Polypropylene is often foam-molded and used as a porous body in order to increase the adhesion amount of microorganisms.
However, since the microorganism-immobilized carrier made of a porous hollow resin has a high surface hydrophobicity and the surface is roughened by means of foam molding or the like for the purpose of facilitating adhesion of bacterial cells, the carrier is not suitable. Immediately after being put into the drainage tank, air bubbles adhered to the surface of the carrier and floated, so that it was difficult to flow when immersed in the drainage, and it took a long time to be able to perform good drainage treatment. .
[0004]
Therefore, many improvements for improving the hydrophilicity of the carrier surface have been proposed. For example, Japanese Patent Application Laid-Open No. 63-302994 discloses that a granular body made of an oxidizable thermoplastic resin is oxidized by contacting with a sulfochrome mixture (sulfuric acid, potassium dichromate and water) or a sulfonated mixture of fuming sulfuric acid. A method of hydrophilizing is disclosed. The carrier made of such oxidized particles improves the interaction with water and suppresses the floating phenomenon of the carrier and the condensation between the carrier bodies.
[0005]
Japanese Patent Application Laid-Open No. 58-198288 discloses a technique for improving the adhesion of microorganisms by forming irregularities on a carrier surface by etching the carrier surface with concentrated sulfuric acid.
[0006]
[Problems to be solved by the invention]
However, since the method for hydrophilizing the carrier surface described above uses a strong oxidizing agent such as concentrated sulfuric acid, there has been a problem that it is dangerous if handling is not performed with great care.
[0007]
Further, as disclosed in JP-A-58-198288, when the treatment is performed under severe conditions such that irregularities are formed on the surface, there is a concern that the carrier is excessively oxidized and a problem in durability occurs.
[0008]
In order to solve these problems, the present invention controls acid treatment conditions within an appropriate range, can be produced simply, inexpensively and safely, has good flowability immediately after use, and has excellent durability. It is an object of the present invention to provide a carrier.
[0009]
[Means for Solving the Problems]
That is, the gist of the present invention resides in a microorganism-immobilized carrier with improved fluidity obtained by treating a molded article containing an acid-modified thermoplastic resin and calcium carbonate with 0.1 N to 5 N hydrochloric acid.
[0010]
Moreover, since the fluidity | liquidity can be improved reliably when the said molded object is immersed in an acid for 0.1 to 10 hours, it is preferable.
Further, it is preferable that the acid is hydrochloric acid because it is excellent in handleability.
In addition, it is preferable that the thermoplastic resin contains an acid-modified thermoplastic resin because the initial fluidity is high, and it is more preferable that the thermoplastic resin further contains a propylene-maleic anhydride copolymer or an ethylene-methacrylic acid copolymer (ionomer resin). preferable.
Moreover, it is preferable that the content of the acid-modified thermoplastic resin in the molded body is 10% by weight or more because the initial fluidity becomes higher.
In addition, it is preferable that the molded body has a hollow cylindrical shape because adhesion of microorganisms is improved.
Moreover, since the fluidity | liquidity improves that the specific gravity of the said molded object is 0.8-1.2 g / cm < 3 >, it is preferable.
In addition, when 100 ml of an apparent volume of the microorganism-immobilized carrier is added to 1 L of a liquid having a solid content of 1000 mg / L and aerated at a flow rate of 1 L / min, the microorganism-immobilized carrier is within 5 hours from the start of aeration. If 80% or more of the water circulates and flows in the liquid, it is preferable because the start-up of the wastewater treatment apparatus starts quickly.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Examples of the present invention will be described below, but the present invention is not construed as being limited thereto.
[0012]
Examples of the thermoplastic resin used in the present invention include, but are not limited to, polypropylene, polyethylene, polyvinyl chloride, ethylene-vinyl acetate copolymer resin, polystyrene, and the like. These thermoplastic resins can be used alone or in combination of two or more, and polypropylene, polyethylene and the like are particularly preferable.
[0013]
It is preferable to use an acid-denatured thermoplastic resin together with the aforementioned thermoplastic resin, since the fluidity of the carrier is further improved. Examples of the acid-modifying thermoplastic resin include propylene-maleic anhydride copolymer (for example, Mitsui Chemicals, trade name Admer, Sanyo Kasei Co., Ltd., trade name Umex, Mitsubishi Chemical Corporation, trade name) Modic), ethylene-methacrylic acid copolymer (ionomer resin, for example, Mitsui DuPont Polychemical Co., Ltd., trade name Himiran), methyl methacrylate-methacrylic acid copolymer (Mitsubishi Rayon Co., Ltd., trade name Acrypet) ) Etc. The acid-modified thermoplastic resin can be used alone or in combination of two or more.
Although the content of the acid-modified polymer depends on the amount of acid modification, it is preferably 10% by weight or more in order to give sufficient hydrophilicity, and the carrier can be obtained with only the acid-modified thermoplastic resin.
[0014]
The molded body used in the present invention may be obtained by molding the above-described resin composition by a well-known method that has been conventionally used. For example, it can be easily manufactured using an extruder, and can be manufactured using special equipment or post-processing. Can also be manufactured at low cost.
At the time of molding, the shape is not necessarily limited and can be a columnar shape, a cylindrical shape, a spherical shape, a cubic shape, or the like. A hollow cylindrical shape is preferable because adhesion of microorganisms is improved.
[0015]
Other components include calcium carbonate, talc, zeolite, barium sulfate, titanium oxide, potassium titanate, aluminum hydroxide, and other specific gravity adjusting materials, azodicarbonamide (ADCA), dinitrosopenta for making porous. Methylenetetramine (DPT), a blowing agent such as carbonic acid, a foaming aid, and further suitable additives may be included.
[0016]
The specific gravity of the molded body used in the present invention is preferably in the range of 0.8 to 1.2 g / cm 3 . Furthermore, from the viewpoint of fluidity in water, a value closer to 1.00 is more desirable. By adjusting the molded body to the above specific gravity, a suitable fluidity can be obtained when a carrier produced using the molded body is used for a fluidized bed.
[0017]
The fluidity of the carrier can be improved by acid-treating the molded body described above with an acid of 0.1 to 5 N. When the concentration of the acid used is less than 0.1 N, the initial fluidity of the carrier is equivalent to that in the case of no treatment, and the effect of the acid treatment is not recognized.
On the other hand, when treated with an acid with a concentration exceeding 5N, the resin surface is likely to erode and dissolve, which may cause problems in durability. In addition, care must be taken during handling. It is not preferable because it is dangerous.
[0018]
The type of acid to be used is not necessarily limited, and sulfuric acid, nitric acid, hydrochloric acid, phosphoric acid, acetic acid, and the like can be used. Among them, hydrochloric acid is preferable because it is inexpensive, has a high treatment effect, and is excellent in handleability.
[0019]
The treatment conditions are not particularly limited as long as the surface of the molded body comes into contact with an acid, but it is preferable to immerse the molded body in an acid solution because it can be easily treated. The temperature for immersion is not particularly limited, and the treatment may be performed at room temperature. The immersion time is preferably 0.1 to 10 hours, and more preferably 0.5 to 5 hours, taking into account the effect of improving the fluidity and the productivity.
In the immersion treatment, it is preferable to stir the liquid because the treatment efficiency is improved.
[0020]
As an evaluation of the fluidity of the microorganism-immobilized carrier, 100 ml of an apparent volume of the microorganism-immobilized carrier is added to 1 L of a liquid having a solid content of 1000 mg / L and aerated at a flow rate of 1 L / min. be able to. In this test, it is preferable that 80% of the microorganism-immobilized carrier circulates in the liquid within 5 hours from the start of aeration. In this fluidity test, the carrier that flows in a short time flows quickly even in an actual apparatus, for example, a biological wastewater treatment apparatus.
The solid content in this fluidity test refers to a substance containing a group of microorganisms capable of metabolizing and decomposing organic components in water, such as activated sludge. Desired. Those that do not have the ability to decompose organic components in water, such as inorganic substances such as sand grains and metal powders, are not included in the solid content in this fluidity test.
[0021]
Hereinafter, embodiments of the present invention will be described in detail with specific examples and comparative examples.
[0022]
1. Manufacturing method of molded body Resin and calcium carbonate are mixed using a biaxial co-directional extruder, molded into pellets, azodicarbonamide is added as a foaming agent, and extrusion molding is performed using a single screw extruder. A porous hollow cylindrical molded body having a diameter of 5 mm, an inner diameter of 3.5 mm, and a length of 5 mm was obtained.
The weight ratio of resin: calcium carbonate: foaming agent was 75: 24: 1.
[0023]
2. Acid treatment The above-mentioned molded body was immersed in an acid solution at 25 ° C. for 2 hours with stirring.
[0024]
3. Fluidity test Using the water treatment apparatus shown in FIG. 1, sludge having an MLSS concentration of 1000 mg / L and a carrier having an apparent volume of 100 ml were added to a 1 liter tank. Then, while aeration of air at 1 L / min, the artificial drainage was used as raw water, and the load was adjusted to 0.4 kg-COD / m3 · day, and the time until the carrier flowed was observed.
[0025]
<Example 1>
Polypropylene was used as the resin, and 3N hydrochloric acid was used as the acid. As a result of the fluidity test, it took 4 hours for 80% of the carrier to flow, and 6 hours for all the carriers to flow.
[0026]
<Example 2>
Propylene-maleic anhydride copolymer was used as the resin, and 3N hydrochloric acid was used as the acid. As a result of the fluidity test, it took 2 hours for 80% of the carrier to flow, and 3 hours for all the carriers to flow.
[0027]
<Example 3>
Ethylene-methacrylic acid copolymer was used as the resin, and 3N hydrochloric acid was used as the acid. As a result of the fluidity test, it took 2 hours for 80% of the carrier to flow, and 5 hours for all the carriers to flow.
[0028]
<Example 4>
Polypropylene was used as the resin, and 1N hydrochloric acid was used as the acid. As a result of the fluidity test, it took 4 hours for 80% of the carrier to flow, and 6 hours for all the carriers to flow.
[0029]
<Comparative Example 1>
Polypropylene was used as the resin, and acid treatment was not performed. As a result of the fluidity test, the time required for 80% of the carrier to flow was 36 hours, and the time required for all the carriers to flow was 48 hours.
[0030]
<Comparative example 2>
Propylene-maleic anhydride copolymer was used as the resin, and no acid treatment was performed. As a result of the fluidity test, the time required for 80% of the carrier to flow was 8 hours, and the time required for all the carriers to flow was 12 hours.
[0031]
<Comparative Example 3>
An ethylene-methacrylic acid copolymer was used as the resin, and no acid treatment was performed. As a result of the fluidity test, it took 8 hours for 80% of the carrier to flow, and 12 hours for all the carriers to flow.
[0032]
As can be seen from the above Examples and Comparative Examples, the fluidity of the carrier could be improved by acid-treating the resin molding.
[0033]
【The invention's effect】
According to the present invention, a carrier having good fluidity and excellent durability can be obtained simply, inexpensively and safely by treating a thermoplastic resin with an acid of 0.1 to 5 N. .
[Brief description of the drawings]
FIG. 1 is a schematic view showing a water treatment apparatus used in Examples.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 Water treatment apparatus 11 Screen 12 Carrier 13 Current plate 14 Aeration pipe

Claims (5)

酸変性熱可塑性樹脂及び炭酸カルシウムを含む成型体を、0.1規定〜5規定の塩酸にて処理してなる流動性が向上した微生物固定化担体。A microorganism-immobilized carrier having improved fluidity obtained by treating a molded article containing an acid-modified thermoplastic resin and calcium carbonate with 0.1 N to 5 N hydrochloric acid. 前記成型体を塩酸に0.1〜10時間浸漬させてなる請求項1記載の微生物固定化担体。  The microorganism-immobilized carrier according to claim 1, wherein the molded body is immersed in hydrochloric acid for 0.1 to 10 hours. 前記酸変性熱可塑性樹脂がプロピレン−無水マレイン酸共重合体を含む請求項1又は2に記載の微生物固定化担体。  The microorganism-immobilized carrier according to claim 1 or 2, wherein the acid-modified thermoplastic resin contains a propylene-maleic anhydride copolymer. 前記酸変性熱可塑性樹脂がエチレン−メタクリル酸共重合体(アイオノマー樹脂)を含む請求項1又は2に記載の微生物固定化担体。  The microorganism-immobilized carrier according to claim 1 or 2, wherein the acid-modified thermoplastic resin contains an ethylene-methacrylic acid copolymer (ionomer resin). 酸変性熱可塑性樹脂から選択される1種以上の樹脂及び炭酸カルシウムを含む成型体を、0.1規定〜5規定の塩酸にて処理してなる、流動性の向上した微生物固定化担体の製造方法。Production of a microorganism-immobilized carrier with improved fluidity obtained by treating a molded body containing one or more kinds of resins selected from acid-modified thermoplastic resins and calcium carbonate with 0.1 N to 5 N hydrochloric acid. Method.
JP2001152331A 2001-05-22 2001-05-22 Microorganism immobilization carrier Expired - Fee Related JP4530320B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001152331A JP4530320B2 (en) 2001-05-22 2001-05-22 Microorganism immobilization carrier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001152331A JP4530320B2 (en) 2001-05-22 2001-05-22 Microorganism immobilization carrier

Publications (3)

Publication Number Publication Date
JP2002346583A JP2002346583A (en) 2002-12-03
JP2002346583A5 JP2002346583A5 (en) 2005-12-02
JP4530320B2 true JP4530320B2 (en) 2010-08-25

Family

ID=18997027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001152331A Expired - Fee Related JP4530320B2 (en) 2001-05-22 2001-05-22 Microorganism immobilization carrier

Country Status (1)

Country Link
JP (1) JP4530320B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006015310A (en) * 2004-07-05 2006-01-19 Nippon Steel Chem Co Ltd Nitrate nitrogen treatment material and method for producing the same

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58198288A (en) * 1982-10-08 1983-11-18 Chiyoda Chem Eng & Constr Co Ltd Particles for attaching microorganisms
FR2612085B1 (en) * 1987-03-13 1989-06-16 Insat GRANULAR WATER TREATMENT MATERIAL AND MANUFACTURING METHOD
JPH05309361A (en) * 1992-04-30 1993-11-22 Tonen Corp Porous medium for water treament
JPH07163992A (en) * 1993-12-14 1995-06-27 Toray Ind Inc Aquatic material and water purification material
JPH09296066A (en) * 1996-05-02 1997-11-18 Ogura Boeki Kk Method for producing microorganism-attached carrier and microorganism-attached carrier
JPH10279724A (en) * 1997-04-03 1998-10-20 Hitachi Chem Co Ltd Method for producing open-cell foam of polyolefin resin
JPH10296284A (en) * 1997-04-30 1998-11-10 Takeda Chem Ind Ltd Carrier for immobilizing microbe and manufacture thereof
JP4414006B2 (en) * 1997-08-22 2010-02-10 日本エンバイロケミカルズ株式会社 Biological treatment carrier
JP4194012B2 (en) * 1999-08-25 2008-12-10 ダイセルノバフォーム株式会社 RESIN COMPOSITION FOR FOAM MOLDED BODY, FOAM MOLDED BODY, AND METHOD FOR PRODUCING THE SAME
JP4489893B2 (en) * 2000-01-28 2010-06-23 日本エンバイロケミカルズ株式会社 Water treatment carrier, method for producing water treatment carrier and water treatment device
JP2001314184A (en) * 2000-02-29 2001-11-13 Sanyo Chem Ind Ltd Carrier for immobilizing microorganism for fluidized bed
JP2001347286A (en) * 2000-06-06 2001-12-18 Rengo Co Ltd Porous hollow article, microorganism immobilizing carrier using the same and method for manufacturing porous hollow article
JP2002219477A (en) * 2001-01-26 2002-08-06 Mitsubishi Rayon Co Ltd Microbial immobilization carrier
JP2002223751A (en) * 2001-01-31 2002-08-13 Mitsubishi Rayon Co Ltd Microbial immobilization carrier

Also Published As

Publication number Publication date
JP2002346583A (en) 2002-12-03

Similar Documents

Publication Publication Date Title
JP3143412B2 (en) Microbial immobilization carrier for fluidized bed
CN113788528B (en) Water treatment micro filler and preparation method thereof
CN111465690A (en) Microbial immobilization carrier
JP4489893B2 (en) Water treatment carrier, method for producing water treatment carrier and water treatment device
JP4530320B2 (en) Microorganism immobilization carrier
US20180179091A1 (en) Solid carbon source, bioreactor having the same and method for wastewater treatment using the same
JP4514874B2 (en) Water treatment carrier, method for producing water treatment carrier and water treatment device
JP2003117577A (en) Microorganism-immobilized carrier, method for producing the same, and wastewater treatment method using the same
JP3587733B2 (en) Microbial carrier and wastewater treatment equipment
JPH09296066A (en) Method for producing microorganism-attached carrier and microorganism-attached carrier
CN112292354A (en) Water treatment method
JPH10180280A (en) Microbial immobilization carrier for water treatment
JP2002223751A (en) Microbial immobilization carrier
JP3761671B2 (en) Carrier for attaching microorganisms
JP4489892B2 (en) Water treatment carrier, method for producing water treatment carrier and water treatment device
JP4722518B2 (en) Microbial carrier for water treatment and production method thereof
CN105668773A (en) Preparation technology of suspended filler for rapid microbial biofilm formation
KR20200092028A (en) Biofilm Core-shell structured particles having biofilm and Method for treating wastewater using same
JP4229426B2 (en) Microorganism immobilization carrier and waste water treatment method using the same
JP5105679B2 (en) Method for producing carrier for water treatment
JP2002219477A (en) Microbial immobilization carrier
JP4597325B2 (en) Mechanically agitated water treatment carrier and mechanically agitated water treatment apparatus
JP3445253B2 (en) Water treatment carrier and water treatment equipment
JP2000210691A (en) Production of carrier for microorganism and carrier for microorganism
JP3455597B2 (en) Fluidized bed wastewater treatment method and apparatus

Legal Events

Date Code Title Description
A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20051013

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20051013

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070713

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081218

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090206

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100114

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20100304

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100401

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100517

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100603

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100604

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130618

Year of fee payment: 3

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130618

Year of fee payment: 3

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130618

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130618

Year of fee payment: 3

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees